The field of photovoltaics generally relates to multi-layer materials that convert sunlight directly into DC electrical power. The basic mechanism for this conversion is the photovoltaic effect, first observed by Antoine-César Becquerel in 1839, and first correctly described by Albert Einstein in a seminal 1905 scientific paper for which he was awarded a Nobel Prize for physics. In the United States, photovoltaic (PV) devices are popularly known as solar cells or PV cells. Solar cells are typically configured as a cooperating sandwich of positive, or p-type and negative, or n-type semiconductors, in which the n-type semiconductor material (on one “side” of the sandwich) exhibits an excess of electrons, and the p-type semiconductor material (on the other “side” of the sandwich) exhibits an excess of holes, each of which signifies the absence of an electron. Near the p-n junction between the two materials, valence electrons from the n-type layer move into neighboring holes in the p-type layer. This creates a carrier depletion zone and a small electrical field in the vicinity of the metallurgical junction that forms the electronic p-n junction. The resulting potential across the junction inhibits further migration of carriers, and any electrons that appear are swept into the n region and any holes that appear are swept into the p region.
When an incident photon excites an electron in the cell into its conduction band, the excited electron becomes unbound from the atoms of the semiconductor, creating a free electron/hole pair. Because, as described above, the p-n junction creates an electric field in the vicinity of the junction, electron/hole pairs created in this manner near the junction tend to separate and move away from junction, with the electron moving toward the n-type side, and the hole moving toward the p-type side of the junction. This creates an overall charge imbalance in the cell, so that if an external conductive path is provided between the two sides of the cell, electrons will move from the n side back to the p side along the external path, creating a useful electric current. In practice, electrons may be collected from at or near the surface of the n side by a conducting grid that covers a portion of the surface, while still allowing sufficient access into the cell by incident photons.
Such a photovoltaic structure, when appropriately located electrical contacts are included, and the cell (or a series of cells) is incorporated into a closed electrical circuit, forms a working PV device. As a standalone device, a single conventional solar cell is not sufficient to power most applications. As a result, solar cells are commonly arranged into PV modules, or “strings,” by connecting the front of one cell to the back of another, thereby adding the voltages of the individual cells together in electrical series. Typically, a significant number of cells are connected in series to achieve a usable voltage. The resulting DC current then may be fed through an inverter, where it is transformed into AC current at an appropriate frequency, which is chosen to match the frequency of AC current supplied by a conventional power grid. In the United States, this frequency is 60 Hertz (Hz), and most other countries provide AC power at either 50 Hz or 60 Hz.
One particular type of solar cell that has been developed for commercial use is a “thin-film” PV cell. In comparison to other types of PV cells, such as crystalline silicon PV cells, thin-film PV cells require less light-absorbing semiconductor material to create a working cell, and thus can reduce processing costs. Thin-film based PV cells also offer reduced cost by employing previously developed deposition techniques for the electrode layers, since similar materials are widely used in the thin-film industry for protective, decorative, and functional coatings. Common examples of low cost commercial thin-film products include water impermeable coatings on polymer-based food packaging, decorative coatings on architectural glass, low emissivity thermal control coatings on residential and commercial glass, and scratch and anti-reflective coatings on eyewear. Adopting or modifying techniques that have been developed in these other fields has allowed a reduction in development costs for PV cell thin-film deposition techniques.
Furthermore, thin-film cells have exhibited efficiencies approaching 20%, which rivals or exceeds the efficiencies of the most efficient crystalline cells. In particular, the semiconductor material copper indium gallium diselenide (CIGS) is stable, has low toxicity, and is truly a thin film, requiring a thickness of less than two microns in a working PV cell. As a result, to date CIGS appears to have demonstrated the greatest potential for high performance, low cost thin-film PV products, and thus for penetrating bulk power generation markets. Other semiconductor variants for thin-film PV technology include copper indium diselenide, copper indium disulfide, copper indium aluminum diselenide, and cadmium telluride.
Some thin-film PV materials may be deposited either on rigid glass substrates, or on flexible substrates. Glass substrates are relatively inexpensive, generally have a coefficient of thermal expansion that is a relatively close match with the CIGS or other absorber layers, and allow for the use of vacuum deposition systems. However, when comparing technology options applicable during the deposition process, rigid substrates suffer from various shortcomings during processing, such as a need for substantial floor space for processing equipment and material storage, expensive and specialized equipment for heating glass uniformly to elevated temperatures at or near the glass annealing temperature, a high potential for substrate fracture with resultant yield loss, and higher heat capacity with resultant higher electricity cost for heating the glass. Furthermore, rigid substrates require increased shipping costs due to the weight and fragile nature of the glass. As a result, the use of glass substrates for the deposition of thin films may not be the best choice for low-cost, large-volume, high-yield, commercial manufacturing of multi-layer functional thin-film materials such as photovoltaics. Therefore, a need exists for improved methods and apparatus for depositing thin-film layers onto a non-rigid, continuous substrate.
a is a flow chart showing exemplary steps in a first method of depositing gallium and indium on a substrate according to the teachings of the present disclosure.
b is a flow chart showing exemplary steps in a second method of depositing gallium and indium on a substrate according to the teachings of the present disclosure.
Manufacture of flexible thin-film PV cells may proceed by a roll-to-roll process. As compared to rigid substrates, roll-to-roll processing of thin flexible substrates allows for the use of relatively compact, less expensive vacuum systems, and of some non-specialized equipment that already has been developed for other thin-film industries. Flexible substrate materials inherently have lower heat capacity than glass, so that the amount of energy required to elevate the temperature is minimized. They also exhibit a relatively high tolerance to rapid heating and cooling and to large thermal gradients, resulting in a low likelihood of fracture or failure during processing. Additionally, once active PV materials are deposited onto flexible substrate materials, the resulting unlaminated cells or strings of cells may be shipped to another facility for lamination and/or assembly into flexible or rigid solar modules. This strategic option both reduces the cost of shipping (due to the use of lightweight flexible substrates vs. glass), and enables the creation of partner-businesses for finishing and marketing PV modules throughout the world. Additional details relating to the composition and manufacture of thin-film PV cells of a type suitable for use with the presently disclosed method and apparatus may be found, for example, in U.S. Pat. No. 7,194,197, to Wendt et al., in patent application Ser. No. 12/424,497, filed Apr. 15, 2009, and in Provisional Patent Application Ser. No. 61/063,257, filed Jan. 31, 2008. These references are hereby incorporated into the present disclosure by reference for all purposes.
Cell 10 is created by starting with a flexible substrate, and then sequentially depositing multiple thin layers of different materials onto the substrate. This assembly may be accomplished through a roll-to-roll process whereby the substrate travels from a pay-out roll to a take-up roll, traveling through a series of deposition regions between the two rolls. The PV material then may be cut to cells of any desired size. The substrate material in a roll-to-roll process is generally thin, flexible, and can tolerate a relatively high-temperature environment. Suitable materials include, for example, a high temperature polymer such as polyimide, or a thin metal such as stainless steel or titanium, among others. Sequential layers typically are deposited onto the substrate in individual processing chambers by various processes such as sputtering, evaporation, vacuum deposition, chemical deposition, and/or printing. These layers may include a molybdenum (Mo) or chromium/molybdenum (Cr/Mo) back contact layer; an absorber layer of material such as copper indium diselenide, copper indium disulfide, copper indium aluminum diselenide, or copper indium gallium diselenide (GIGS); a buffer layer or layers such as a layer of cadmium sulfide (CdS); and a transparent conducting oxide (TCO) layer acting as the top electrode of the PV cell. In addition, a conductive current collection grid, usually constructed primarily from silver (Ag) or some other conductive metal, is typically applied over the TCO layer.
Although the precise thickness of each layer of a thin-film PV cell depends on the exact choice of materials and on the particular application process chosen for forming each layer, exemplary materials, thicknesses and methods of application of each layer described above are as follows, proceeding in typical order of application of each layer onto the substrate:
The remainder of this disclosure focuses on various methods and apparatus for forming a semiconductor absorber layer on an underlying substrate web.
This section describes various general considerations regarding formation of a thin-film absorber layer on a substrate web. The absorber layer typically is p-type semiconductor in the form of copper-indium-gallium-diselenide (CIGS) or its readily acceptable counterpart, copper-indium-diselenide (CIS). Other materials, such as copper indium disulfide or copper indium aluminum diselenide, also may be used. These different compositions, among others, can be used essentially interchangeably as an absorber layer in various embodiments of the present teachings, depending on the particular properties desired in the final product. For convenience and specificity, the remainder of this disclosure occasionally may refer to the absorber layer as a CIGS layer. However, it should be understood that some or all of the present teachings also may be applied to various other suitable absorber layer compositions.
The strip material, or substrate web, feeds in the direction of arrow 25 from a pay-out roll 60 to a downstream take-up roll 68 within chamber 24. As the strip material moves through chamber 24, the p-type absorber layer is formed on the bottom surface of the substrate web (as depicted in
Within chamber 24, and specifically within deposition region R, a molten-liquid-to-vapor co-evaporation process for establishing a p-type semiconductor layer is performed. Chamber 24 is designed specifically for the creation of a CIGS layer, as opposed, for example, to a CIS layer. Accordingly, structures 70, 72, 74, 76, 78, 79 and 81 function to generate vapors of copper (70), gallium (72), indium (74) and selenium (76, 78, 79, 81) for deposition onto the moving substrate web. Structures 70-81 form the bulk of the vapor-deposition-creating system, generally indicated at 83, of the present embodiment. The vapor deposition environment created in deposition region R may provide a continuum of evaporant fluxes. Within region R, effusion fluxes may be held approximately constant, and by translating the substrate web over the sources, the substrate may encounter a varying flux of material specifically designed to achieve optimum performance in the CIGS layer.
Blocks 70, 72 and 74, which relate to the vapor-delivery of copper, gallium, and indium, respectively, represent heated effusion sources for generating plumes of vapor derived from these three materials. Each of these effusion sources may include: (1) an outer thermal control shield; (2) a boat, reservoir, or crucible containing the associated molten copper, gallium, or indium; (3) a lid that covers the associated case and reservoir, and that contains one or more vapor-ejection nozzles (or effusion ports) per crucible to assist in creating vapor plumes; and (4) a specially designed and placed heater located near the effusion ports, or in some embodiments formed integrally with the ports.
Structures 76, 78, 79 and 81 represent portions of a selenium delivery system that creates a background selenium gas pressure in some or all parts of the deposition region. A selenium delivery system may deliver selenium directly through one or more orifices in a local Se source. Alternatively, in the embodiment of
The processing rate using a roll-to-roll deposition approach is limited only by the web translation rate through the deposition region, and by the web width. The web translation rate is set by the minimum time required for sufficient film deposition, which is determined by the details of the reactions that occur inside the deposition region. The maximum web width is limited by the requirement of sufficiently uniform composition and thickness across the width and, as a practical matter, also may be limited by the availability of sufficiently wide rolls of suitable substrate material, such as 25 μm-thick stainless steel. Some vacuum coating techniques, including evaporative techniques used for CIGS deposition and described in the present disclosure, rely on evaporation sources that use arrays of orifices, or effusion ports, arranged to provide sufficiently uniform deposition. Deposition uniformity across the width of the web (concurrent with sufficient material deposition) can be achieved if the effusion ports are spaced across the web width, and if the mass flow of each effusion port is well-controlled.
This section relates to systems and methods for depositing a thin-film p-type semiconductor layer onto a substrate in a specific exemplary multi-zone deposition process. As described previously and depicted schematically in
In the exemplary procedure of
Each of the six deposition zones described in this section may have a similar basic structure but may vary as to number, deposition material and location within the zone, of material sources. Each zone may include at least two material sources, for example the material sources shown in
In some zones, such as in the zone depicted in
Each deposition zone may be enclosed within a separate solid enclosure 101. Generally, each enclosure 101 may surround the associated deposition zone substantially completely, except for an aperture in the top portion of the enclosure over which the moving substrate web passes. This allows separation of the deposition zones from each other, providing the best possible control over parameters such as temperature and selenium pressure within each zone.
The exemplary chamber 100 of
Specifically, first zone 110 may be configured to deposit a layer of sodium fluoride (NaFl) onto the web. The presence of sodium is believed to improve p-type carrier concentration by compensating for defects in one or more of the subsequently deposited CIGS layers, and thus to improve the overall efficiency of the PV cell. An initial layer of NaFl has been found to be optimal. Alternatively, potassium (K) or lithium (Li) may serve a similar purpose as sodium. Furthermore, other compounds aside from NaFl, such as sodium selenide (Na2Se2), sodium selenite (Na2SeO3), sodium selenate (Na2O4Se), or other similar compounds incorporating potassium and/or lithium, also may be suitable for improving p-type carrier concentration.
Second zone 112, which is shown in isolation in
GI (more specifically GI selenide) may be deposited through the nearly simultaneous—but separate—deposition of gallium and indium onto the same portion of the moving web. As indicated in
Selenium source 118 is configured to provide selenium gas to second zone 112, and similar selenium sources may also be located in the third, fifth, sixth and/or seventh zones within chamber 100 to provide selenium gas to the third, fifth, sixth and/or seventh zones within chamber 100, up to a pressure in the range of approximately 700-2000 μTorr. Each selenium source in a zone may be independently monitored and controlled. Providing a background of selenium gas results in deposition of selenium along with the other source materials, such as GI, such that the deposited layer may comprise indium-gallium selenide, gallium selenide or gallium-rich indium-gallium selenide.
As shown in more detail in
Each deposition zone may itself be enclosed within a separate solid enclosure 101. Generally, each enclosure 101 may surround the associated deposition zone, for example second zone 112, substantially completely, except for an aperture 101a in the top portion of enclosure 101, over which the moving substrate web passes. This allows separation of the deposition zones from each other, providing the best possible control over parameters such as temperature and selenium pressure within each zone. Aperture 101a in the top portion of enclosure 101 may have a width that is substantially the same as the width of substrate web 102.
A deposition material is liquefied or otherwise disposed within the body portion 120 of a given source, and emitted at a controlled temperature in plumes of evaporated material through effusion ports 124. As described previously, because the angular flux of material emitted from an effusion port 124 with a particular geometry is a function primarily of temperature of the port and/or deposition material, this allows for control over the thickness and uniformity of the deposited layers created by the vapor plumes.
As shown in
Sources of copper material may disposed within the third zone 126 relatively close to the entrant side of the substrate web 102 into the third zone 126, but alternatively may be disposed more toward the egress side of the third zone 126 with similar effect. However, by providing the copper sources relatively close to the entrant side of the third zone 126, the copper atoms have slightly more time to diffuse through the underlying layers prior to deposition of subsequent layers, and this may lead to preferable electronic properties of the final CIGS layer.
Fourth zone 128 may be configured as a sensing zone, in which one or more sensors, generally indicated at 130, monitor the thickness, uniformity, or other properties of some or all of the previously deposited material layers. Typically, such sensors may be used to monitor and control the effective thickness of the previously deposited copper, indium and gallium on the web, by adjusting the temperature of the appropriate deposition sources in the downstream zones and/or the upstream zones in response to variations in detected thickness. To monitor properties of the web across its entire width, two or more sensors may be used, corresponding to the two or more sources of each applied material that span the width of the web disposed substantially symmetrically across the transverse dimension of the web. Fourth zone 128 is described in more detail below with reference to
Fifth zone 132 may be configured to deposit a second layer of copper, which may have somewhat lesser thickness than the copper layer deposited in third zone 126, from a pair of sources disposed substantially symmetrically across the transverse dimension of the web. Similar to the copper sources described in third zone 126, two copper sources within fifth zone 132 may be configured to emit copper plumes from multiple effusion ports spanning the width of the substrate web. Furthermore, the copper sources may be disposed on the entrant side of the fifth zone 132 to allow relatively more time between copper deposition and subsequent layer deposition. Fifth zone 132 may also include a selenium source.
Sixth zone 134 may be configured to deposit a second layer of gallium-indium onto the web. In construction, sixth zone 134 may be similar to second zone 112. The thickness of the gallium-indium layer deposited in sixth zone 134 may be small relative to the thickness of the GI layer deposited in second zone 112. In sixth zone 134, gallium and indium may be emitted at somewhat lesser effusion temperatures relative to the effusion temperatures of the gallium and indium emitted in second zone 112. These relatively lower temperatures result in lower effusion rates, and thus to a relatively thinner layer of deposited material. Such relatively low effusion rates may allow fine control over ratios such as the copper to gallium+indium ratio (Cu:Ga+In) and the gallium to gallium+indium ratio (Ga:Ga+In) near the p-n junction, each of which can affect the electronic properties of the resulting PV cell. As in the second zone 112, gallium may be emitted slightly earlier along the web path than indium, to promote better adhesion to the underlying layers of molecules.
Seventh zone 136 may be similar in construction to one or both of second zone 112 and sixth zone 134 and may be configured to deposit a third slow-growth, high quality layer of gallium-indium (GI) onto the substrate web. In some embodiments, this final deposition zone and/or GI layer may be omitted from the deposition process, or a layer of indium alone may be deposited in seventh zone 136. As in sixth zone 134, application of a relatively thin, carefully controlled layer of gallium and/or indium allows control over ratios such as (Cu:Ga+In) and (Ga:Ga+In) near the p-n junction. This may have a beneficial impact on the efficiency of the cell by, for example, allowing fine-tuning of the electronic band gap throughout the thickness of the CIGS layer. Furthermore, the final layer of GI is the last layer applied to complete formation of the p-type CIGS semiconductor, and it has been found beneficial to form a thin layer of GI having a relatively low defect density adjacent to the p-n junction that will be subsequently formed upon further application of an n-type semiconductor layer on top of the CIGS layer.
As shown in
This basic structure, with at least two independently operable heated sources containing the same deposition material spanning the web width, may be common to each of the zones of chamber 100 in which material is deposited onto the web (deposition zones 110, 112, 126, 132, 134 and 136). By providing two independent sources of material disposed substantially symmetrically across the width of the web, the thickness of each deposited material may be independently monitored on each side of the web, and the temperature of each source may be independently adjusted in response. This allows a wider web to be used, leading to a corresponding gain in processing speed per unit area, without compromising material thickness uniformity.
IV. Optimizing Layer Composition with Mixed Sources
As noted above, ratios such as the copper to gallium+indium ratio and the gallium to gallium+indium ratio (“GGI”) in the CIGS layer can affect the electronic properties of the resulting PV cell. Accordingly, achieving control over these ratios is desirable in a CIGS deposition system.
More specifically, the GGI ratio throughout the CIGS film thickness is a strong determinant of solar cell efficiency.
achieving a GGI ratio between 0.25 and 0.35 in region 2;
a GGI “well” 0.4 to 0.5 μm below the surface of the CIGS layer;
a mild slope towards the back of the CIGS coating (i.e., in regions 3 and 4);
a maximum GGI ratio of between 0.40 and 0.50; and
a modest decline in the GGI ratio in region 4.
As described previously, one method of attempting to control the GGI ratio as a function of depth is to use independently controllable gallium and indium sources. According to the teachings of this section, another method is to mix gallium and indium inside a single source (or inside multiple sources), which may preferably be disposed in the last deposition zones through which a moving substrate web passes (zones 6 and/or 7 as described in the previous section). It is preferable to have finer control of the deposition of gallium and indium in these later zones because, as the thin film deposition process nears its end, less time is available for solid state diffusion to occur after layers are deposited. Thus, controlled mixing of the source materials prior to deposition is desirable, especially in these final zones.
In a mixed source, at least two possible mixing methods may be used. In a first method, indium and gallium are mixed prior to evaporation, forming a continuous solution in the melt. This first method will generally be referred to as “pre-mixing.” In a second method, separate crucibles containing gallium or indium may be used in a single source, with resulting indium and gallium vapors being mixed in a manifold prior to exiting through the source's effusion port(s). This second method will generally be referred to as “vapor-mixing.” In either method, the vapor pressures of the individual elements (and their evaporation behavior) are largely preserved in the resulting alloy.
When a mixed source is used, indium and gallium vapors leaving the source are generally well mixed throughout the entire deposition zone. As a result, mixtures can be accomplished which result in a nearly constant GGI ratio over substrate web lengths greater than 500 meters, and process control can be maintained. In addition, using mixed mixing indium and gallium sources yields flatter GGI profiles through the CIGS coating and more uniform profiles across the web width. In particular, a GGI ratio between 0.25 and 0.35 at the film surface typically can be achieved by this approach. To facilitate uniformity of the GGI ratio, multiple sources mixing indium and gallium may be disposed across the width of the substrate web, as depicted generally in
In addition to a single mixed indium gallium source, a plurality of mixed sources or sources containing only indium or gallium may be added to the deposition system, and may result in even finer control of the GGI profile by adding another degree of freedom. Control over the GGI ratio may be more straightforward if only one of the sources is a mixed source. Accordingly, the following configurations of mixed and/or single material sources may be used in the terminal CIGS deposition zones:
a. Ga, (In,Ga)
b. (In, Ga), In
c. (In,Ga), (In,Ga)
d. (In, Ga) only
When multiple mixed sources are used (as in option (c) above), the first source the substrate is exposed to will typically have a smaller GGI ratio than the second source.
Another possible implementation of a single mixed indium and gallium source is earlier in the deposition process, i.e. not necessarily in the terminal deposition zones. This may be useful because the GGI profile near the back contact (regions 3 and 4 in
a. (In,Ga), In
b. (In, Ga) only
In the case of a single mixed indium gallium source at the beginning of CIGS deposition, reaction kinetics may lead to a natural decreasing gradient in the GGI ratio, with a higher ratio near the back contact region, as desired.
When using one or more mixed indium gallium sources, it remains important to precisely control the amount of source material deposited on the substrate web. In a first, or pre-mixing option, this control may be generally accomplished by controlling the ratio of the gallium and indium used in the mixture. For simplicity, consider the case of only a single pre-mixed indium gallium source installed in the final CIGS deposition zone to supply all indium and gallium necessary to complete the final stage of the CIGS deposition process. The ratio of indium to gallium (and thus the GGI ratio) that effuses from the mixed source is determined by the charge mixture and the temperature at which the source is operated. However, the source temperature cannot affect the ratio independent of the total amount of indium and gallium effusing. Furthermore, the charge mixture typically cannot be modified once the system is evacuated and the deposition process is initiated. Therefore, it is desirable to know the relationships between the melt composition within a mixed source, the composition of the mixed vapor effused by the source, and the composition of the mixed film that actually adheres to the substrate.
For an efficient solar cell, there is a range of acceptable GGI ratios deposited during the final stage of the CIGS deposition process. This preferred range is approximately 10% to 45%, as indicated by lines 302 and 304 in
As described above, in a process using a pre-mixed indium gallium source, the relative amounts of indium and gallium are based on how the source was charged. Therefore, the optimal control strategy with a pre-mixed source is to charge the source precisely with desired masses of indium and gallium, and to use the total number of molecules of indium and gallium deposited onto the substrate web from the mixed source as the process control variable for the effusion from that source.
In the second, or vapor-mixing option, where gallium and indium are located in separate crucibles within the source, gallium and indium vapors are mixed in a manifold or chamber and the ratio of gallium and indium may be controlled using independent heating for each crucible. This method has resulted in even finer control of the GGI ratio, due to different evaporation characteristics of each source material. Use of a mixing manifold allows better outcome control and more complete mixing of gallium and indium than does use of non-mixed sources where the process must rely on plume overlap and diffusion in the applied layers.
Heater plate 408 may be substantially rectangular and planar, with suitable recesses and openings further described below. Heater plate 408 may also include one or more bores 412 for suitably housing measuring devices such as thermocouples. Additionally, heater plate 408 may include thermal breaks, such as thermal break 414, which are narrow slots milled out of the solid material of heater plate 408. Thermal break 414 is appropriately sized to minimize thermal conduction from one side of heater plate 408 to the other without significant loss of structural strength, thus facilitating independent temperature control for each crucible.
First heating element 416 may be located within first recess 420 and second heating element 418 may be located within second recess 422 in heater plate 408. First heating element 416 and second heating element 418 may be single-piece heating elements which provide heating to vaporize source material in first crucible 402 and second crucible 404, respectively. First heating element 416 and second heating element 418 may also form one or more nozzles 424 through which vaporized source material may flow. Because nozzles 424 are formed by first heating element 416 and second heating element 418, heating of the vapor may be maintained until the vapor exits vapor-mixing source 400 completely. Examples of integrated heater/nozzle configurations are described in U.S. patent application Ser. No. 12/424,497, filed Apr. 15, 2009 which is incorporated herein by reference.
Vapor-mixing source 400 also includes sealing and thermal insulation layer 426 (not pictured), which may be configured to completely cover integrated assembly 406 with the exception of the effusion ports, or outlets, of nozzles 424 and any other openings required to allow access for devices such as instrument cables, electrical connections, and structural support members. Sealing and thermal insulation layer 426 may be any suitable material configured to provide thermal insulation and to substantially seal manifold chamber 410. Typically, a top seal is created using flexible grafoil (a carbon-based sheet-like material also used for high temperature gasket applications). The grafoil is die-cut to fit the top of heater plate 408, with cut-outs for nozzles 424. Layers of grafelt (a carbon-based fibrous high temperature thermal insulation) are then typically stacked to a suitable height, and a final layer of grafoil may be utilized to provide containment. The resulting stack of grafoil, grafelt, heating elements, integrated assembly 406, and crucibles may be clamped or otherwise connected together to maintain seals at all mating surfaces. Sealing and thermal insulation layer 426 may have any appropriate thickness such that suitable thermal insulation is provided without impeding vapor flow from the effusion ports of nozzles 424.
As depicted in
Exemplary types of sensors suitable for use in monitoring stations 130 and 140 may include one or more of X-Ray Florescence (XRF), Atomic Absorption Spectroscopy (AAS), Parallel Diffraction Spectroscopic Ellipsometry (PDSE), IR reflectometry, Electron Impact Emission Spectroscopy (EIES), in-situ x-ray diffraction (XRD) both glancing angle and conventional, in-situ time-resolved photoluminescence (TRPL), in-situ spectroscopic reflectometry, in-situ Kelvin Probe for surface potential, and in-situ monitoring of emissivity for process endpoint detection. One or more computers (not shown) may be configured to analyze data from the monitoring station to monitor a property, such as thickness, of deposited layers, and subsequently to adjust the effusion rates and/or temperatures of a corresponding material source or crucible.
When mixed indium and gallium sources are used, the computer(s) used in conjunction with the monitoring stations may be configured to convert the measured thicknesses of indium and gallium to a total number of molecules deposited per unit area (e.g., using the density and molecular weight of gallium and indium). Determining the total amount of deposited material in this manner allows the deposited GGI ratio to be determined. Accurate control of the mixed source then may be attained by providing temperature adjustments to the mixed source(s) in response to the measured ratio.
a shows a flow chart depicting an exemplary method for depositing a gallium and indium layer according to the pre-mixing method of the current teachings. In a first step 502, gallium and indium may be mixed in a single crucible or container. Exact proportions of gallium and indium may be utilized, with a preferred ratio in the range previously discussed, and thoroughly mixed by any suitable means. For example, proper quantities of gallium and indium, in solid shot or bead form, may be weighed into a container and stirred by hand with a small rod made of an inert material. T typically, the resulting eutectic mixture will exist in a liquid or semi-liquid state at room temperature. In step 504, the crucible may be heated to evaporate the mixed source material. Heating may be accomplished by any suitable method, including one or more electrical heating elements. As previously described and shown in
b shows a flow chart depicting an exemplary method for depositing a gallium and indium layer according to the vapor-mixing method of the current teachings. In a first step 514, gallium and indium may be provided in separate crucibles or containers. In step 516, each crucible may be heated to evaporate the source material. Heating may be accomplished by any suitable method, including one or more electrical heating elements configured to heat the crucibles together or independently. Independent heating of each crucible is preferred, as it results in finer adjustment and control of the resulting vapor composition. In step 518, the resulting indium and gallium vapors may be combined in a suitable chamber configured to facilitate mixing of the vapors. Following this mixing, in step 520 the mixed vapor may be deposited onto a suitable substrate. As before, this may be accomplished using a process already described, wherein a moving substrate web transported in roll-to-roll fashion passes over a source, and a layer of mixed gallium and indium vapor is deposited. Thickness of the deposited layer in this step may be substantially controlled by speed of web transport and heating of source material, and GGI ratio may be controlled by adjustment of each crucible's temperature and evaporation rate. In step 522, the deposited layer may be measured to determine whether desirable characteristics have been attained or maintained, whether adjustments have been successful, or whether the process is properly in control. This measurement may be accomplished, for example, at a suitable monitoring station utilizing instruments as previously described. In step 524, the results of measurement in step 522 may be analyzed by any processor configured to determine the characteristics of the deposited layer(s), to compare those characteristics to desired values, and to provide an output signal to cause adjustments calculated to bring the characteristics of the deposited layer(s) within desired parameters. This output signal may include automatic adjustment of heating, web transport speed, and/or human-readable displays, alarms, and/or warnings. In step 526, the heating of the source materials may be adjusted to bring the characteristics of the deposited layer(s) within desired parameters. Use of one or more non-mixed gallium or indium sources may be employed such that this adjustment of heating of the source materials may include altering the temperature of one or more non-mixed sources instead of or in addition to the mixed sources.
The methods, systems, and devices described in this disclosure have been exemplified with respect to deposition of gallium and indium. The same or similar principals may be useful for depositing other materials to produce photovoltaic devices. For example mixing schemes and configurations described herein may be used to deposit combinations of tellurium and cadmium, or copper, zinc, and tin. It should also be appreciated that the same principals may be applied to deposit mixtures of more than two substances. For example, a manifold may be configured to receive, mix, and effuse three or more substances from three or more sources, each with independent temperature control.
The disclosure set forth above may encompass multiple distinct inventions with independent utility. Although each of these inventions has been disclosed in its preferred form(s), the specific embodiments thereof as disclosed and illustrated herein are not to be considered in a limiting sense, because numerous variations are possible. The subject matter of the inventions includes all novel and nonobvious combinations and subcombinations of the various elements, features, functions, and/or properties disclosed herein. For various thin layer deposition applications, different combinations of deposition steps and zones may be used in addition to the specific deposition zone configurations described above. None of the particular steps included in the examples described and illustrated are essential for every application. The order, combination, and number of steps and/or components may be varied for different purposes. Other variables may be controlled via the described monitoring stations, for example speed of web transport, pressure, selenium gas output, web temperature, etc. It may be desirable to use various numbers, combinations, and arrangements of crucibles, mixing manifolds, nozzles, and heating elements for differing applications.
This application is a continuation of U.S. patent application Ser. No. 14/194,407, filed Feb. 28, 2014, which is a continuation of U.S. patent application Ser. No. 12/980,185, filed Dec. 28, 2010, which claims priority under 35 U.S.C. §119 and applicable foreign and international law of U.S. Provisional Patent Application Ser. No. 61/284,925, filed Dec. 28, 2009, which is hereby incorporated by reference in its entirety. Also incorporated by reference in their entireties are the following patent and patent application: Pat. No. 7,194,197, Ser. No. 12/424,497 filed Apr. 15, 2009.
Number | Date | Country | |
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61284925 | Dec 2009 | US |
Number | Date | Country | |
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Parent | 14194407 | Feb 2014 | US |
Child | 14688776 | US | |
Parent | 12980185 | Dec 2010 | US |
Child | 14194407 | US |